Fermentation apparatus

A fermentation apparatus comprising:

• (a) a fermentor vessel shell having a hollow interior chamber adapted to contain fluid therein, said vessel having upper and lower end portions and an inner and outer vessel diameter;
• (b) heat exchange means disposed in said vessel, wherein said heat exchange means comprises a plurality of baffles, wherein each of said baffles comprise a plurality of parallel tubes, each of which tubes having a first end and a second end, wherein each of said baffles is equipped with
• (i) an inlet header means for introducing heat exchange fluid into each of said baffles, in open communication with the first end of said parallel tubes, and
• (ii) an outlet header means for removing heat exchange fluid from each of said baffles, in open communication with the second end of said parallel tubes;
• wherein the plurality of baffles are positioned within said vessel so as to define an inner heat exchange diameter and an outer heat exchange diameter wherein said inner heat exchange diameter defines an unobstructed zone occupying in the range of about 30 up to 60% of the total internal fermentor vessel diameter and said outer heat exchange means diameter is no greater than the inner diameter of said vessel;
• wherein the axis of the parallel tubes of said plurality of baffles is parallel to the longitudinal axis of said fermentor vessel;
• wherein each of said plurality of baffles is positioned at an angle, .alpha., with respect to the radial projection from the longitudinal axis of the fermentation vessel to the point where the longitudinal axis of the parallel tube rows intersects the inner diameter of the vessel, wherein .alpha. ranges from 5.degree. up to 30.degree.;
• (c) first inlet means for the introduction of nutrient media and carbon and energy source into said fermentor vessel;
• (d) agitation means comprising
• (i) a shaft centrally positioned within said fermentor vessel and coaxially aligned with the longitudinal axis of said fermentor vessel,
• (ii) drive means attached to said shaft, and
• (iii) a plurality of impellers mounted on said shaft;
• wherein the diameter of said impellers is no greater than the unobstructed zone defined by the inner heat exchange diameter;
• wherein at least the bottom-most impeller is mounted on said stirring shaft in the lower end portion of said vessel;
• (e) second inlet means for the introduction of gas into said fermentor vessel comprising a sparging means having a face side with a plurality of holes therein;
• wherein said sparging means is positioned symmetrically in the fermentor vessel with respect to the longitudinal axis of said fermentor vessel;
• wherein the diameter of said sparging means is no greater than the diameter of said impellers;
• and wherein the face side of said sparging means is positioned parallel to, and within 1/3 to 1/10 impeller diameters from, the bottom edge of the bottom-most impeller of said plurality of impellers;
• (f) outlet means for the removal of ferment from the lower end portion of said fermentor vessel;
• and
• (g) means for degassing foam mounted on the upper portion of said fermentor vessel and positioned on the outer perimeter thereof.